• Applied Chemistry for Engineering
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• v.7 no.2
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• pp.280-288
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• 1996

In the ozone evolution using $PbO_2$, which was electrodeposited on Ti plate at various conditions in electrolyte, the effects of lead dioxide structure on the current efficiency and surface structure changes of lead dioxide were investigated. Also the effects of oxygen transfer reaction on the ozone evolution were investigated by means of a $PbO_2$ electrodeposited on the platinum rotating disk electrode. In order to develope an electrode for ozone evolution, durability of lead dioxide and optimum current density were investigated. At the electrodeposited lead dioxide with the larger grain size and higher crystallinity, the efficiency for ozone evolution was higher. Optimum current density to electrodeposite lead dioxide with large grain size and high crystalinity was $50mA/cm^2$. Lead dioxide deposited in the presence of glycerin showed the best advantage of ozone evolution. Also lead dioxide electrodeposited at less than $10mA/cm^2$ or at more than $100mA/cm^2$ has poor performance of ozone evolution and poor adhesive strength to substrate. In the beginning of ozone evolution, surface structure of lead dioxide was changed and this change resulted in good effects on ozone evolution. Lead dioxide doped with other elements was favorable not to ozone evolution but to oxygen evolution, so it is speculated that ozone evolution has not intermediate stage of oxygen evolution and occurs competitively with oxygen evolution. When ozone was evolved at $0.7{\sim}0.8A/cm^2$, the current efficiency was highest.

• Proceedings of the Korean Society of Propulsion Engineers Conference
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• 2006.11a
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• pp.150-153
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• 2006

Gas generator should be adopted either fuel rich or oxidizer rich combustion because of the temperature restriction to avoid any possible thermal damages to turbine blade. This study focuses to model the non-equilibrium chemical reaction of kerosene/LOx with detailed kinetics developed by Dagaut using Perfectly stirred reactor(PSR) assumption. To predict more reliable species fraction and other gas properties, Frenklach's soot model was added to Dagaut's detailed kinetics.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2013.05a
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• pp.104-104
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• 2013

고분자이면서 유전체인 Poly-Tetra-Fluoro-Ethylene (PTFE) 튜브에 AC형 고전압을 인가하여 유전체 장벽 방전 (dielectric barrier discharge, DBD)를 유도하고, 발생된 마이크로 플라즈마에 의한 PTFE 튜브 내벽의 표면 개질에 관한 연구이다. 가스인입과 진공배기가 가능한 장치에 PTFE 튜브를 연결하고, 튜브내부를 진공상태를 유지하면서 반응가스를 이용하여 튜브 내벽을 표면개질 하였다. 반응가스를 아르곤, 수소, 아세틸렌, 산소, 질소를 반응 단계에 맞게 혼입하여 마이크로 플라즈마를 발생시켜 플라즈마에 의한 표면변화를 관찰하였다. 표면은 반응성 가스 플라즈마에 의해 물리 화학적 반응이 일어나 고분자 표면의 반응성 활성화를 통한 표면개질의 방식으로 진행되었다. 표면 개질된 튜브 내벽 표면에 대해 XPS, FT-IR, SEM, 접촉각 측정과 분석 실시함으로써 표면변화를 관찰하였다.

• Proceeding of EDISON Challenge
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• 2016.03a
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• pp.273-276
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• 2016

최근 single-layer $MoSe_2$와 같은 2차원의 TMD 화합물들이 물분해 광촉매로서 각광받고 있다. TMD 화합물 중 single-layer $MoSe_2$는 수소 발생 반응을 일으킬 수 있으나 산소 발생 반응은 일으킬 수 없어 산화 반응을 진행시킬 추가적인 전극이 필요하다. 이 연구에서는 strain과 doping을 통해 valence band를 아래로 이동시켜 $MoSe_2$를 더 좋은 물분해 광촉매로 변화시키는 방법을 모색하였다. 먼저 Armchair, zigzag, biaxial isotropic, z-axis direction으로 strain을 걸어줄 때 전자구조의 변화를 관찰하였다. z-axis 방향으로 -2.5% strain을 걸어주었을 때 VBM이 0.07eV만큼 감소하였다. 또한 Mo를 Nb로 치환하고 Se를 P, As로 치환한 다음 전자구조를 관찰하였다. Nb와 doping의 경우 VBM이 감소함을 확인하였으며 As doping의 경우 산화반응이 일어날 수 있고 산화력과 환원력이 비슷해짐을 알아내었다. 또한 산화반응과 환원반응이 일어나는 위치가 분리됨을 확인하였다.

• Journal of the Korea Organic Resources Recycling Association
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• v.18 no.1
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• pp.66-72
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• 2010

This study was done to analyze the condition of combustion exhaust gas that is produced according to incinerator operating condition in A area Kyonggido. The boiler exhaust gas temperature, the oxygen concentration of boiler, the outgassing temperature of Semi Drying Sorber(SDS), the temperature of catalytic reactor, the concentration of NOx, SOx, CO, Hcl and Dust were investigated by change the temperature of incinerator. The concentration of SOx, CO, HCL and DUST were below 5 ppm as increase the temperature of incinerator however the concentration of NOx was increased from 40 ppm to 70 ppm as increase the temperature of incinerator. The boiler exhaust gas temperature and the temperature of catalytic reactor were not changed however the oxygen concentration of boiler was decreased gradually as increase the temperature of incinerator.

• Journal of Soil and Groundwater Environment
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• v.7 no.3
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• pp.95-102
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• 2002

Manganese oxide/ hydrogen peroxide($MnO_2$/${H_2}{O_2}$) reactions were investigated as an alternative to Fenton-like reaction to reduce chlorinated organic compounds in groundwater This system showed high degradation of CT with low ${H_2}{O_2}$concentration($\leq$294mM) at neutral condition, and CT degradation increased with increasing pH values. The rate of CT degradation was not so much dependent on increase in $MnO_2$concentration since increase in production of oxygen during the reaction obstructed reaction of ${H_2}{O_2}$ on the surface of $MnO_2$. These results show that $MnO_2$catalyzed Ponton-like reaction could be a potential alternative method for treating chlorinated organic compounds in groundwater.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2015.05a
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• pp.192-193
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• 2015

음극방식은 피방식체를 일정 전위로 음극분극 하는 원리로써 외부전원을 인가하거나 비전위의 금속을 희생양극으로 연결하여 방식하는 방법이다. 해수 중에서 음극방식을 실시할 경우 음극 표면에 용존산소 환원반응과 수소발생반응이 일어나 $OH^-$ 이온이 발생하게 된다. 이러한 반응에 의해 생성되는 석회질 피막 (Calcareous deposit)은 강구조물의 부식방지를 위한 물리적인 방호벽 역할을 하면서 용존산소의 확산 및 이동을 억제하며, 전류밀도를 감소시킨다. Potentiostat 및 rectifier를 이용하여 정전위 및 정전류 조건에서 형성된 석회질 피막을 SEM, EDS, XRD를 통해 분석하고 이를 바탕으로 양극의 종류(Al, Zn) 및 1, 5, $10mA/m^2$의 전류밀도 조건에서 실제 강관에 형성된 석회질 피막의 메커니즘을 해명하였다. 또한 석회질 피막 형성 시 Steel Wire Mesh를 설치하여 그 영향에 대해서도 분석하였다. 석회질 피막의 내구성은 침지-자연전위 및 밀착성 테스트를 통해 평가되었다.

• Korean Journal of Organic Agriculture
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• v.20 no.4
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• pp.703-713
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• 2012

Three types of aeration system were installed in experimental liquid fertilization tanks to investigate the change of characteristics of pig slurry used as a raw material for making livestock liquid fertilizer. The aeration systems of the reaction tanks were composed of three major part: the air suppling part (blower), the air pipe part, and the air diffuser part. In the first tank (reactor A), the air was supplied from the bottom of the reaction tank through air pipe system connecting air diffuser with commercial ordinary blower. In the second tank (reactor B), the air diffuser was located 10cm above the bottom of the reactor. In the third tank (reactor C), the pure air was supplied with circulating pjg slurry. The oxygen content of pure air was about 90%. The pure air was mixed with pig slurry by mechanically in the air suppling part (blower) and the air pipe part. The agitation effect was highest in the reactor C than other reactors. The contents of SS, COD, T-N and T-P of each samples collected at middle part of all reactors were 8,500, 4,188, 694 and 422mg/L; 9,000, 4,247, 813 and 356mg/L; 8,667, 6,910, 973 and 269mg/L, respectively.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2003.05a
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• pp.117-121
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• 2003

SBR과 SBBR 모두 대부분의 유기물은 포기기간에 소모되었으며, SBBR의 경우 부족한 유기물 조건에서도 원활한 탈질화 반응이 일어난 것을 볼 때, 유기물 농도가 낮은 우리나라의 하수에 적합한 공정으로 생각된다. 질산화 속도에 있어서는 유기물과 용존산소의 접촉기회에 있어 유리한 조건을 가진 SBR이 더 크게 나타났다. 그러나 탈질화 반응에 있어서는 SBBR이 더 높은 것으로 나타났다. SBR의 경우 높은 $NO_3$의 존재로 인해 1차 비포기 기간중 인의 방출은 거의 발생하지 않았으나, SBBR의 경우 1차 비포기 기간에 인 방출과 1차 포기기간에 인 섭취가 일어났다.

• Clean Technology
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• v.19 no.4
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• pp.416-422
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• 2013

In environmental friendly aspects, the synthesis of glycerol carbonate from glycerol using carbon monoxide and oxygen gases which were produced in petrochemical plants was studied. The oxidative carbonylation of glycerol under batch reaction system was performed on parameter conditions such as effect of various metals (Cu, Pd, Fe, Sn, Zn, Cr), oxidizing agents, mole ratio of carbon monoxide to oxygen, catalyst amount, solvent types, reaction temperature and time and dehydrating agents. In particular copper chloride catalysts showed the excellent activities, and the glycerol carbonate yields over CuCl and $CuCl_2$ catalysts were the maximum of 44% and 64%, respectively at the following reaction conditions: solvent as nitrobenzene, mole ratio of 1:3:0.15 (glycerol:carbon monoxide:catalyst), mole ratio of 2:1 (carbon monoxide:oxygen), the total pressure of 30 bar at 413 K for 4 hr. It was found that reactivity were significantly different depending on the oxidation number of Cu catalysts, and oxygen plays an important role as oxidizing agents in producing H2O during oxidation reaction after carbonylation of glycerol.